CN204224603U - A kind of holothurian oral liquid production enzymolysis device - Google Patents
A kind of holothurian oral liquid production enzymolysis device Download PDFInfo
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- CN204224603U CN204224603U CN201420704023.6U CN201420704023U CN204224603U CN 204224603 U CN204224603 U CN 204224603U CN 201420704023 U CN201420704023 U CN 201420704023U CN 204224603 U CN204224603 U CN 204224603U
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Abstract
A kind of holothurian oral liquid production enzymolysis device, comprise enzymatic vessel and heat exchange box, enzymatic vessel is provided with by motor-driven stir shaft, stir shaft is provided with stirring rake, enzymatic vessel is provided with material inlet and material outlet, enzymatic vessel is provided with interlayer, heat exchange box is connected with cold water pipe, heat transfer tube is provided with in heat exchange box, the two ends of heat transfer tube are connected with inlet pipe I and muffler I respectively, heat exchange box is connected with the hot water inlet of interlayer lower end by hot water inlet pipe, hot water inlet pipe is provided with pump and valve, the upper end of interlayer is provided with hot water outlet, hot water outlet is connected with heat exchange box by hot water return pipe, the upper end of interlayer is also provided with inlet mouth, inlet mouth is connected with inlet pipe II, inlet pipe II is provided with valve, the lower end of interlayer is provided with air outlet, air outlet is connected with muffler II, muffler II is provided with valve, inlet pipe I is all connected with boiler with inlet pipe II, muffler I is connected with boiler with muffler II, heat exchange box is provided with temperature gauge.
Description
Technical field
The utility model relates to the technical field that holothurian oral liquid is produced, particularly a kind of holothurian oral liquid production enzymolysis device.
Background technology
Sea cucumber is one of marine organisms of high nutritive value, is rich in a large amount of protein and polysaccharide isoreactivity material, can be used as after being ill, tonic that postpartum etc. is first-selected.Although sea cucumber delicious flavour and nutritive ingredient high, it is difficult to preserve, price is high, so present eaten sea cucumber mostly is dry product, dry product eats the problem that there is nutrition leak in trouble and production process.In order to solve the problem existing for dry Stichopus japonicus, people have invented the method making holothurian oral liquid, enzymolysis is needed in the process making holothurian oral liquid, need after enzymolysis to kill ferment treatment, existing enzymatic vessel, generally adopt high-temperature vapor directly to add in the interlayer of enzymatic vessel to heat, but in the process of sea cucumber enzymolysis, need the temperature range controlled to be 50 DEG C ~ 60 DEG C, direct high-temperature vapor heats, because the temperature of high-temperature vapor is higher, hydrolysis temperature is wayward, once hydrolysis temperature is more than 60 DEG C, the activity of enzyme will be affected, the efficiency of enzymolysis will reduce, affect production efficiency.The weak point that Here it is existing for prior art.
Summary of the invention
Technical problem to be solved in the utility model, is exactly for the deficiency existing for prior art, and provides a kind of holothurian oral liquid production enzymolysis device, while can effectively avoiding rainwater to enter in cabinet, can also effectively carry out dispelling the heat and pressure release.
This programme is achieved by the following technical measures: a kind of holothurian oral liquid production enzymolysis device, comprise enzymatic vessel, described enzymatic vessel is provided with by motor-driven stir shaft, described stir shaft is provided with at least one group of stirring rake, described enzymatic vessel is provided with material inlet and material outlet, described enzymatic vessel is provided with interlayer, also comprise heat exchange box, described heat exchange box is connected with cold water pipe, heat transfer tube is provided with in described heat exchange box, the two ends of described heat transfer tube are connected with inlet pipe I and muffler I respectively, described cold water pipe and inlet pipe I are provided with valve, described heat exchange box is connected with the hot water inlet of interlayer lower end by hot water inlet pipe, described hot water inlet pipe is provided with pump and valve, the upper end of described interlayer is provided with hot water outlet, described hot water outlet is connected with heat exchange box by hot water return pipe, the upper end of described interlayer is also provided with inlet mouth, described inlet mouth is connected with inlet pipe II, described inlet pipe II is provided with valve, the lower end of described interlayer is provided with air outlet, described air outlet is connected with muffler II, described muffler II is provided with valve, described inlet pipe I is all connected with boiler with inlet pipe II, described muffler I is all connected with boiler with muffler II, described heat exchange box is provided with temperature gauge.
The technical characteristic of this programme also comprises: above-mentioned enzymatic vessel upper end is provided with venting hole, and described venting hole is provided with air-filtering membrane.Adopt this programme, arrange venting hole and can discharge the gas produced in enzymolysis process, the air-filtering membrane of setting can prevent impurity from entering contaminated material in enzymatic vessel.
The technical characteristic of this programme also comprises: above-mentioned heat transfer tube comprises many row's U-shaped pipes.
The technical characteristic of this programme also comprises: above-mentioned heat exchange box is provided with thermal insulation layer.Adopt this programme, heat exchange box can be avoided externally to shed heat.
The technical characteristic of this programme also comprises: above-mentioned interlayer is provided with temperature gauge.The temperature gauge arranged can measure the temperature in interlayer, makes it meet enzymatic hydrolysis condition.
The technical characteristic of this programme also comprises: above-mentioned enzymatic vessel is provided with temperature gauge.The temperature gauge arranged can measure the temperature in enzymatic vessel, makes it meet enzymatic hydrolysis condition.
The technical characteristic of this programme also comprises: above-mentioned hot water return pipe is provided with valve.
The technical characteristic of this programme also comprises: above-mentioned cold water pipe is connected with cooling column.
The beneficial effects of the utility model can be learnt from above-mentioned technical scheme: a kind of holothurian oral liquid production enzymolysis device, comprise enzymatic vessel, described enzymatic vessel is provided with by motor-driven stir shaft, described stir shaft is provided with at least one group of stirring rake, described enzymatic vessel is provided with material inlet and material outlet, described enzymatic vessel is provided with interlayer, also comprise heat exchange box, described heat exchange box is connected with cold water pipe, heat transfer tube is provided with in described heat exchange box, the two ends of described heat transfer tube are connected with inlet pipe I and muffler I respectively, described cold water pipe and inlet pipe I are provided with valve, described heat exchange box is connected with the hot water inlet of interlayer lower end by hot water inlet pipe, described hot water inlet pipe is provided with pump and valve, the upper end of described interlayer is provided with hot water outlet, described hot water outlet is connected with heat exchange box by hot water return pipe, the upper end of described interlayer is also provided with inlet mouth, described inlet mouth is connected with inlet pipe II, described inlet pipe II is provided with valve, the lower end of described interlayer is provided with air outlet, described air outlet is connected with muffler II, described muffler II is provided with valve, described inlet pipe I is all connected with boiler with inlet pipe II, described muffler I is all connected with boiler with muffler II, described heat exchange box is provided with temperature gauge.Hydrolysis temperature general control in sea cucumber production process is between 50 DEG C ~ 60 DEG C, high-temperature vapor heat transfer tube is passed into by the cool water heating squeezed in heat exchange box becomes the hot water of about 65 DEG C from cold water pipe from inlet pipe I, hot water in heat exchange box is squeezed in the interlayer of enzymatic vessel by hot water inlet pipe by pump, under the pressure effect of pump, hot water in interlayer can to enter heat exchange box through superheated water return pipe from hot water outlet and realize hot water circulation heated and meet temperature needed for enzymolysis, after enzymolysis completes, hot water cooled via return air pipe II in interlayer can be flowed into boiler, from inlet pipe II, be filled with high-temperature vapor again the ferment treatment that goes out is heated to enzymatic vessel, high-temperature water vapor flows into boiler by muffler II, heat is recycled, adopt this enzymolysis device can meet enzymolysis and go out enzyme time different demands to temperature, enhance productivity.
As can be seen here, the utility model compared with prior art, has substantive distinguishing features and progress, and its beneficial effect implemented also is apparent.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure: 1-enzymatic vessel, 2-motor, 3-stir shaft, 4-stirring rake, 5-interlayer, 6-material inlet, 7-material outlet, 8-valve, 9-hot water inlet, 10-heat exchange box, 11-inlet pipe I, 12-valve, 13-cold water pipe, 14-valve, 15-hot water inlet pipe, 16-pump, 17-valve, 18-hot water return pipe, 19-valve, 20-hot water outlet, 21-inlet mouth, 22-inlet pipe II, 23-valve, 24-heat transfer tube, 25-muffler I, 26-air outlet, 27-muffler II, 28-valve, 29-temperature gauge, 30-temperature gauge, 31-temperature gauge, 32-thermal insulation layer, 33-venting hole.
Embodiment
For the technical characterstic of this programme can be clearly demonstrated, below by embodiment, and in conjunction with its accompanying drawing, this programme is set forth.
As shown in the figure, a kind of holothurian oral liquid production enzymolysis device, comprise enzymatic vessel 1, described enzymatic vessel 1 is provided with the stir shaft 3 driven by motor 2, described stir shaft 3 is provided with three groups of stirring rakes 4, described enzymatic vessel 1 is provided with material inlet 6 and material outlet 7, described enzymatic vessel 1 is provided with interlayer 5, also comprise heat exchange box 10, described heat exchange box 10 is connected with cold water pipe 13, heat transfer tube 24 is provided with in described heat exchange box 10, the two ends of described heat transfer tube 24 are connected with inlet pipe I 11 and muffler I 25 respectively, described cold water pipe 13 is provided with valve 14, described inlet pipe I 11 is provided with valve 12, described heat exchange box 10 is connected by the hot water inlet 9 of hot water inlet pipe 15 with interlayer 5 lower end, described hot water inlet pipe 15 is provided with pump 16 and valve 17, the upper end of described interlayer 5 is provided with hot water outlet 20, described hot water outlet 20 is connected with heat exchange box 10 by hot water return pipe 18, the upper end of described interlayer 5 is also provided with inlet mouth 21, described inlet mouth 21 is connected with inlet pipe II 22, described inlet pipe II 22 is provided with valve 23, the lower end of described interlayer 5 is provided with air outlet 26, described air outlet 26 is connected with muffler II 27, described muffler II 27 is provided with valve 28, described inlet pipe I 11 is all connected with boiler (not shown) with inlet pipe II 22, described boiler can provide high-temperature vapor, described muffler I 25 is all connected with boiler with muffler II 27, described cold water pipe 13 is connected with cooling column (not shown), described cooling column can provide cold water, described heat exchange box 10 is provided with temperature gauge 31.
Described enzymatic vessel 1 upper end is provided with venting hole 33, and described venting hole 33 is provided with air-filtering membrane, arranges venting hole 33 and can discharge the gas produced in enzymolysis process, and the air-filtering membrane of setting can prevent impurity from entering contaminated material in enzymatic vessel 1.
Described heat transfer tube 24 comprises many row's U-shaped pipes.
Described heat exchange box 10 is provided with thermal insulation layer 32, and described thermal insulation layer 32 can adopt common cystose, and heat exchange box 10 can be avoided externally to shed heat.
Described interlayer 5 is provided with temperature gauge 29, and the temperature gauge 29 of setting can measure the temperature in interlayer 5, makes it meet enzymatic hydrolysis condition.
Described enzymatic vessel 1 is provided with temperature gauge 30, and the temperature gauge 30 of setting can measure the temperature in enzymatic vessel 1, makes it meet enzymatic hydrolysis condition.
Described hot water return pipe 18 is provided with valve 19.
Hydrolysis temperature general control in sea cucumber production process is between 50 DEG C ~ 60 DEG C, the high-temperature vapor passed into heat transfer tube 24 from inlet pipe I 11 will become about 65 DEG C hot water from cold water pipe 13 cool water heating squeezed in heat exchange box 10, hot water in heat exchange box 10 is squeezed in the interlayer 5 of enzymatic vessel 1 by hot water inlet pipe 15 by pump 16, under the pressure effect of pump 16, hot water in interlayer 5 can to enter heat exchange box 10 through superheated water return pipe 18 from hot water outlet 20 and realize hot water circulation heated and meet temperature needed for enzymolysis, now, valve 17, valve 19 is opened, valve 8 and valve 28 are closed, after enzymolysis completes, valve 28 can be opened the hot water cooled via return air pipe II 27 in interlayer 5 is flowed into boiler, valve-off 17 again, valve 8 and valve 19, open valve 23 and valve 28 from inlet pipe II 22, to be filled with high-temperature vapor to go out ferment treatment to enzymatic vessel 1 heating, high-temperature vapor flows into boiler by muffler II 27, heat is recycled, adopt this enzymolysis device can meet enzymolysis and go out enzyme time different demands to temperature, enhance productivity.
Can pass through without the technical characteristic described in the utility model or adopt existing techniques in realizing; do not repeat them here; certainly; above-mentioned explanation is not to restriction of the present utility model; the utility model is also not limited in above-mentioned embodiment; the change that those of ordinary skill in the art makes in essential scope of the present utility model, remodeling, interpolation or replacement, also should belong to protection domain of the present utility model.
Claims (8)
1. a holothurian oral liquid production enzymolysis device, comprise enzymatic vessel, described enzymatic vessel is provided with by motor-driven stir shaft, described stir shaft is provided with at least one group of stirring rake, described enzymatic vessel is provided with material inlet and material outlet, described enzymatic vessel is provided with interlayer, it is characterized in that: also comprise heat exchange box, described heat exchange box is connected with cold water pipe, heat transfer tube is provided with in described heat exchange box, the two ends of described heat transfer tube are connected with inlet pipe I and muffler I respectively, described cold water pipe and inlet pipe I are provided with valve, described heat exchange box is connected with the hot water inlet of interlayer lower end by hot water inlet pipe, described hot water inlet pipe is provided with pump and valve, the upper end of described interlayer is provided with hot water outlet, described hot water outlet is connected with heat exchange box by hot water return pipe, the upper end of described interlayer is also provided with inlet mouth, described inlet mouth is connected with inlet pipe II, described inlet pipe II is provided with valve, the lower end of described interlayer is provided with air outlet, described air outlet is connected with muffler II, described muffler II is provided with valve, described inlet pipe I is all connected with boiler with inlet pipe II, described muffler I is all connected with boiler with muffler II, described heat exchange box is provided with temperature gauge.
2. holothurian oral liquid production enzymolysis device according to claim 1, is characterized in that: described enzymatic vessel upper end is provided with venting hole, and described venting hole is provided with air-filtering membrane.
3. holothurian oral liquid production enzymolysis device according to claim 2, is characterized in that: described heat transfer tube comprises many row's U-shaped pipes.
4. holothurian oral liquid production enzymolysis device according to claim 3, is characterized in that: described heat exchange box is provided with thermal insulation layer.
5. holothurian oral liquid production enzymolysis device according to claim 4, is characterized in that: described interlayer is provided with temperature gauge.
6. holothurian oral liquid production enzymolysis device according to claim 5, is characterized in that: described enzymatic vessel is provided with temperature gauge.
7. holothurian oral liquid production enzymolysis device according to claim 6, is characterized in that: described hot water return pipe is provided with valve.
8. the holothurian oral liquid production enzymolysis device according to claim 1 or 2 or 3 or 4 or 5 or 6 or 7, is characterized in that: described cold water pipe is connected with cooling column.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420704023.6U CN204224603U (en) | 2014-11-21 | 2014-11-21 | A kind of holothurian oral liquid production enzymolysis device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420704023.6U CN204224603U (en) | 2014-11-21 | 2014-11-21 | A kind of holothurian oral liquid production enzymolysis device |
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| CN204224603U true CN204224603U (en) | 2015-03-25 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111920749A (en) * | 2020-08-31 | 2020-11-13 | 滕明军 | Face essence containing quinophthalol and preparation method thereof |
| CN112715897A (en) * | 2019-10-14 | 2021-04-30 | 江西巨荣生物科技有限公司 | Solidified enzyme honey and preparation method thereof |
| CN115349574A (en) * | 2022-09-07 | 2022-11-18 | 杭州佰倍优生物科技有限公司 | Albumin polypeptide ultrafiltration system and device for inhibiting hydrolysis and removing bitter taste |
-
2014
- 2014-11-21 CN CN201420704023.6U patent/CN204224603U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112715897A (en) * | 2019-10-14 | 2021-04-30 | 江西巨荣生物科技有限公司 | Solidified enzyme honey and preparation method thereof |
| CN111920749A (en) * | 2020-08-31 | 2020-11-13 | 滕明军 | Face essence containing quinophthalol and preparation method thereof |
| CN115349574A (en) * | 2022-09-07 | 2022-11-18 | 杭州佰倍优生物科技有限公司 | Albumin polypeptide ultrafiltration system and device for inhibiting hydrolysis and removing bitter taste |
| CN115349574B (en) * | 2022-09-07 | 2023-08-18 | 杭州佰倍优生物科技有限公司 | Albumin polypeptide ultrafiltration system and device for inhibiting hydrolysis and removing bitter taste |
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| C14 | Grant of patent or utility model | ||
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| CP01 | Change in the name or title of a patent holder |
Address after: 265600 Shandong city of Yantai province Penglai city Chong Road Economic Development Zone No. 168 Patentee after: PENGLAI MARINE (SHANDONG) CO., LTD. Address before: 265600 Shandong city of Yantai province Penglai city Chong Road Economic Development Zone No. 168 Patentee before: Marine Organism Co., Ltd., Penglai City |